Expanded bed adsorption at production scale: Scale-up verification, process example and sanitization of column and adsorbent

1997 ◽  
Vol 16 (2) ◽  
pp. 57 ◽  
Author(s):  
A.-K. Barnfield Frej ◽  
H. J. Johansson ◽  
S. Johansson ◽  
P. Leijon
2005 ◽  
Vol 93 (1) ◽  
pp. 14-20 ◽  
Author(s):  
Peter Brixius ◽  
Inger Mollerup ◽  
Ole Elvang Jensen ◽  
Markus Halfar ◽  
Jörg Thömmes ◽  
...  

2006 ◽  
Vol 50 (3) ◽  
pp. 275-281 ◽  
Author(s):  
Evelien L. van Boxtel ◽  
Gerrit A. van Koningsveld ◽  
Stef J. Koppelman ◽  
Lambertus A. M. van den Broek ◽  
Alfons G. J. Voragen ◽  
...  

1999 ◽  
Vol 34 (2) ◽  
pp. 159-165 ◽  
Author(s):  
J. Feuser ◽  
M. Halfar ◽  
D. Lütkemeyer ◽  
N. Ameskamp ◽  
M.-R. Kula ◽  
...  

2009 ◽  
Vol 52 (2) ◽  
pp. 427-436 ◽  
Author(s):  
João Batista Severo Jr. ◽  
Roberto Rodrigues de Souza ◽  
José Carlos Curvelo Santana ◽  
Elias Basile Tambourgi

In the present work, the effect of bed expansion on BSA adsorption on Amberlite IRA 410 ion-exchange resin was studied. The hydrodynamic behavior of an expanded bed adsorption column on effects of the biomolecules and salt addition and temperature were studied to optimize the conditions for BSA recovery on ion-exchange resin. Residence time distribution showed that HEPT, axial dispersion and the Pecletl number increased with temperature and bed height, bed voidage and linear velocity. The binding capacity of the resin increased with bed height. The Amberlite IRA 410 ion-exchange showed an affinity for BSA with a recovery yield of 78.36 % of total protein.


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